Enhancement of flow rates through porous media

ABSTRACT

For extracting a liquid (such as oil) from a porous medium, the liquid is subjected to pulses that propagate through the liquid flowing through the pores of the medium. The pulses cause momentary surges in the velocity of the liquid, which keeps the pores open. The pulses can be generated in the production well, or in a separate excitation well. If the pulses travel with the liquid, the velocity of travel of the liquid through the pores can be increased. The solid matrix is kept stationary, and the pulses move through the liquid. The pulses in the liquid can be generated directly in the liquid, or indirectly in the liquid via a localised area of the solid matrix.

GENERAL DESCRIPTION OF THE INVENTION

This invention relates to the dynamic enhancement of fluid flow rates ina porous medium, using pressure and strain pulsing. The inventionrelates to devices and methods designed to explicitly enhance the flowrate of fluids (liquids or gases) and mixtures of fluids and solids(e.g. oil and sand particles) in porous media by means of application ofpressure pulsing or strain pulsing to the region of flow. The pressurepulsing is applied to the liquid phase of a porous medium throughperiodic cycling of liquid volumes by mechanical, hydraulic, orpneumatic devices at one or more points. Strain pulsing can similarly beapplied through mechanical or electromechanical excitation. The twoprocesses are intimately linked in that a pressure pulse generates astrain pulse, and vice-versa. Dynamic enhancement of fluid flow rate canbe applied to the following technologies:

Flow of liquids or liquid-solid mixtures to wellbores in petroleum orwater extraction processes from porous media.

Flow of liquids or liquid-solid mixtures in porous media to wells, sumpsor other pressure sinks during cleaning of contaminated shallow aquiferscomprised of sand, gravel, or fractured rock.

Flow of liquids or liquid-solid mixtures in contained or natural porousmedia beds used for chemical engineering reaction processes, filtration,refining, cleaning, or other processes where liquids or liquid-solidmixtures are flowing from one point to another under the effect of apressure or gravity-induced gradient.

LIST OF THE DRAWINGS

FIG. 1 is a section of a porous medium;

FIG. 2 is a diagram of an apparatus for demonstrating dynamicenhancement of flow rate through the medium of FIG. 1;

FIG. 3 is a graph of a fluid flow rate enhancement, without entrainedsolids;

FIG. 4 is a graph of a fluid flow rate enhancement, with entrainedsolids;

FIG. 5 is a graph showing pressure pulse transmission through the porousspecimen;

FIG. 6: Strain Pulse Flow Enhancement Apparatus

FIG. 7a is a plan view of a field implementation for oil production;

FIG. 7b is a section on line Y—Y of FIG. 7a;

FIG. 8 is an implementation of flow enhancement in horizontal wells;

FIG. 9 is a section of a pressure pulsing device;

FIG. 10a is a section of a well having a strain-pulsing device;

FIG. 10b is a section of a strain-pulsing device in a well;

FIG. 10c is a cross-section of a portion of the device of FIG. 10a;

FIG. 11 is a section of a vibrational enhancement device located at theground surface;

FIG. 12 is a section through a reaction bed of granular material;

FIG. 13 is a section of an installation for creating pulses, producingoil, and monitoring the production;

FIG. 14a is a graph of the velocity of liquid passing through a pore ina porous medium, with pulses;

FIG. 14b is a corresponding graph to FIG. 14a, when the pulses are at adifferent frequency.

1 DEFINITIONS

In the context of this specification, a porous medium is a natural orman-made material comprising a solid matrix and an interconnected pore(or fracture) system within the matrix. The pores are open to each otherand can contain a fluid, and fluid pressure can be transmitted and fluidflow can take place through the pores. Examples of natural materialsinclude gravels, sands and clays; sandstones, limestones and othersedimentary rocks; and fractured rocks including fractured sedimentaryrocks which have both fractures and pores through which fluids may flow.Examples of man-made porous media include filtration beds of natural orartificial granular materials or manufactured solid porous materials, aswell as beds of catalysts used to accelerate reactions between fluidphases or fluid-solid phases during refining, chemical synthesis, orother processes. Structures such as tailings dikes, dams, fluid rechargeor filtration beds, and so on, can be regarded as porous media.

The porosity of a porous medium is the ratio of the volume of open spacein the pores to the total volume of the medium Systems of practicalinterest in the present context have porosities that lie in the range 5%to 60%.

The porosity (pore, fractures, and channels) is filled with fluids,which may be gases or liquids or a combination of the two. Liquids canbe oil, water (with dissolved constituents), or man-made liquids such asgasoline, chlorinated bi-phenyls, polymers, and non-aqueous phaseliquids deliberately or accidentally introduced into the porous medium.Gases may be natural hydrocarbons, air, carbon dioxide, or man-madegaseous products introduced deliberately or accidentally into the porousmedium.

All porous media are characterized by a permeability. Permeability is anaverage measure of the geometry of the pores, pore throats, and otherproperties which describes the flow rate of fluids through the mediumunder the effect of a pressure gradient or a gravity force inducedbecause of differences in density among fluid phases or solid-fluidphases.

Pressure pulsing is a deliberate variation of the fluid pressure in theporous medium through the injection of fluid, withdrawal of fluid, or acombination of alternating periods of injection and withdrawal. Thepressure pulsing may be regular or irregular (periodic or aperiodic),continuous or episodic, and it may be applied at the point of withdrawalor at other points in the region of the porous medium affected by theflow process.

Strain pulsing is a deliberate variation of the strain at a point orlocal region in the porous medium by applying changes in strain througha device which vibrates, oscillates, or which expands and contracts involume. The strain pulsing may be regular or irregular, continuous orepisodic, and it may be applied at the point of withdrawal or at otherpoints in the region of the porous medium affected by the flow process.

Dilational and shear pulses are the two basic types of excitation. In adilational pulse, the perturbation is isotropic (equal in alldirections) at the point of application, and may be termed a volumetricpulse. Pressure pulsing is dominantly a dilational perturbation. Thedilational perturbation moves out in all directions approximatelyequally and is subject to scattering phenomena. In a shear pulse, arelative lateral excitation is applied so that the energy imparted tothe porous medium is dominated by shear motion, such as occurs when slipoccurs along a plane. Shear perturbation is highly anisotropic, and thedistribution of energy depends on the orientation of the perturbingsource. Shear perturbations can therefore in principle be focussed sothat more energy propagates in one direction than in another. Strainpulsing can be anisotropic or isotropic, depending on the nature of theexcitation source.

Flow takes place in a porous medium through generating a pressuregradient in the mobile (moveable) phases by creating spatial differencesin fluid pressures. Reducing or increasing the pressure at a number ofpoints may generate this by the withdrawal or injection of fluids. Itmay also be generated through the force of gravity acting upon fluids ofdifferent density, such as oil, formation water, gas or air, injectednon-aqueous phase liquids and other fluids. In a system where the solidparticles are partly free to move, density differences between solidsand fluids may also lead to gravity-induced flow.

In a porous medium containing two or more non-miscible fluids (oil andwater for example), the wetting phase is that gas or liquid which,because of surface tension and wettability effects, is in contact withthe majority of the solid material. It forms the pendular fluid contactsbetween grains in a granular porous medium, and coats the walls of flowchannels (FIG. 1). The non-wetting phase is that gas or liquid whichlies in the interstices and channels and is separated from the solidmaterial by a film of the wetting phase fluid. In FIG. 1, the mineralgrains 1 are coated with a wetting liquid 2, while a non-wetting liquid3 occupies the rest of the pore space. The pore throat dimension 4,averaged through the medium, is important in dictating the velocity atwhich liquid can pass through the pores 5 of the medium.

The non-wetting phase 3 might be continuous or discontinuous. If it iscontinuous, then an interconnected and uninterrupted path of that liquidexists in the medium. If it is discontinuous, the non-wetting phase mayexist as isolated droplets or regions, which are nowhere in directphysical contact with other regions of the same phase.

2 Evidence of Dynamic Enhancement of Fluid Flow

There exist in the public literature observations of increased flowrates in oil wells and water wells during and after dynamic excitationfrom earthquakes or other events which can create sufficient strain inthe medium to affect the porosity, and the through-flow velocity of theliquid, even in a minuscule manner.

In the systems as described herein, periodic or irregular pressurepulsing in a flowing system under a pressure gradient increases the flowrate of the mobile phase toward the extraction point.

Field observations confirm that a porosity perturbation applied to apetroleum well enhances flow to the well for some time thereafter byincreasing the mobility of the fluid phase. In the case of a petroleumwell producing fluid and sand, a general increase in the mobility of thecomplex solid-liquid-gas flowing phase takes place. The perturbation inthese cases may also be a single sharp pressure pulse applied at theproduction well.

Theoretical developments and field observations show that fluid flowrate to a producing water well or petroleum well is enhanced if theliquid-flow-borne solids are allowed to enter the wellbore in anunimpeded manner. This is analogous to a porosity diffusion process inthat a porosity change occurs as the solid phase is produced along withthe liquids. This porosity change slowly propagates out from theproduction point into the porous medium through a diffusive mechanism,and is accompanied by changes in the pressure and pressure gradient withtime and location around the wellbore. In the oil industry, the processof allowing the sand to flow unimpeded is called cold production, coldflow, or sand production.

In general, the flow enhancement accompanying any porosity diffusionprocess takes place in a system with a pressure gradient, and theprocesses preferentially increase flow rates of the mobile, non-wettingphase if more than one fluid is present as a continuous phase.

One feature of the invention lies in the recognition that dynamicexcitation through application of a pressure pulse, a strain pulse, or aseries of pulses anywhere in the flowing porous medium can enhance theflow rate. Fluid rate enhancement occurs at the exit points of a givensystem (wellbore, reaction bed, and pipeline), that are also the pointsof low pressure in the medium. Furthermore, we have recognised that thefluid flow enhancement can be theoretically predicted and analysed,measured in the laboratory, and physically explained.

In addition to the porosity diffusion effect and the enhancement in flowrate that it generates, dynamic excitation has several other beneficialeffects on production performance of wells. The dynamic excitation maybe induced as a pressure pulse or a strain pulse, generated by apulsating or vibrating source. Excitation may be periodic or aperiodic,continuous or episodic, and applied in the stratum or at the surface,provided that sufficient porosity diffusion amplitude is transmitted tothe region of interest.

The permeability of a conventional producing well can be impaired by themigration and consequent accumulation in the near-wellbore environmentof fine-grained solid particles, which can pass through the pore throatconstrictions in the porous medium. When, as described herein, theporous medium is being dynamically excited the tendency for theseparticles to bridge and block porosity is substantially reduced, thusallowing the well to maintain flowing conditions with a minimum ofimpairment.

Particularly in viscous heavy oils but also in some conventional oils,certain liquids (asphaltenes in general) can be precipitated as smallsize solid particles when the liquid encounters the lower pressures nearthe wellbore. These particles can accumulate in the pore throats,impairing the permeability of the system and reducing the flow rate tothe producing well. Dynamic excitation, as described herein, providescyclic strain energy aimed at mitigating the tendency for blockages ofthese precipitants, maintaining the well in a superior flowingcondition.

Finally, under conditions where the granular particles of the porousmedium are allowed to flow along with the fluids (as in sandproduction), the flowing particles may bridge together near thewellbore, forming a stable sand arch, and stop the solids flow. Thiscondition leads to a massive deterioration in the fluid productivity ofthe well. Dynamic excitation, as described herein, provides aperturbation energy, which tends to destabilize these arches because ofthe small cyclic strains induced at the contacts between sand grains.

3 Experimental Verification

FIG. 2 shows an experimental set-up 20 to demonstrate the physicalprinciple of dynamic enhancement of fluid flow. The cylindrical device23 contains a dense sand pack 24, which is under an applied stress of1.5 MPa. The sand pack is flushed through with paraffin oil (or anyother wetting phase) to coat the grains as a continuous wetting phase.Then, glycerin (or other non-miscible liquid) is allowed to flow throughthe sand and form a continuous non-wetting phase that is immiscible withthe wetting phase. The fluid exit port 25 allows production under theaction of a pressure gradient maintained constant by keeping a reservoir26 of the mobile non-wetting phase liquid 27 at an elevation higher thanthe device 23. Exit port 25 has a screen 28 between the port 25 and thesand pack 24 for experiments where the sand is not allowed to flow;however, for experiments where the sand is permitted to flow, the screenis removed.

The flow experiment is allowed to reach a condition of steady-state exitport flow rate Q. Once this condition is reached, a dynamic perturbationis applied to the system by one of two methods: a small strain pulse isapplied through a transducer embedded in the sand 24; or, a periodicpulse is applied to the upstream part of the device by perturbing theflexible flow lines manually or automatically (at point 29). The varyingexcitation is indicated by the symbol in the circle. Pressuretransducers (P1, P2, and P3) are electronic devices designed to monitorany changes in pressure in the system induced by the dynamic excitation.The sand pack 24 is maintained in compression by hydraulic pistons 35.

The strain pulse is applied through a small acoustic transducer linkedto an oscilloscope and signal generator 30. The acoustic transducer (notshown in FIG. 2) is embedded in the sand 24 during the assembly of theexperiment. It has a diameter of 15 mm and is encased in latex to sealit from the fluid and to provide good coupling with the sand pack. Beingof such small size with respect to the cell, it does not impede the flowof liquids through the experimental apparatus. The frequency of thesonic pulse was varied from 10 Hz to 60 Hz during the excitation periodin the experiments. The period of excitation is indicated in FIG. 3 aspulsing-started 32 to pulsing-stopped 34. In between periods ofexcitation, no pulsing takes place, but flow is allowed to continue;this is necessary to evaluate flow enhancement through contrastingperiods of excitation and periods of no excitation, in the sameapparatus without other changes on the pressure head or flow properties.

The pressure pulsing is applied by manually squeezing the upstreamflexible tube 29 connecting the fluid reservoir 26 to the top of theflow apparatus. This manual squeezing is applied at a frequency of 0.5to 2 Hz continuously during the excitation period.

FIG. 3 demonstrates quantitatively the change in the flow rate from theexperimental device. The lower line 36 is the steady flow at a hydraulichead of 0.25 meters (the top of the fluid in the reservoir wasmaintained at an elevation of 0.25 meters above the entry port). Thisline 36 is to demonstrate that without pressure or strain pulsing, noflow enhancement takes place. The upper line 37 is the demonstration ofenhancement. In this case, the fluid reservoir was maintained 0.5 metersabove the fluid entrance port, and one may note that the slope of thenon-pulsed portions of the line 38 is almost exactly twice the slope ofthe lower line 36. This is in accordance with the conventional view offlow through porous media: a doubling of the hydraulic head withoutpulsing leads to a doubling of the flow rate.

The slope of the upper line without pressure pulsing or strain pulsing(38) is approx 2.67 cm3/min. With pressure pulsing or strain pulsing,the flow rate increases (37) to approx 5.7 cm3/min, an enhancementfactor of about 2.15. Various experiments conducted with differentexcitation frequencies and excitation times showed flow rate enhancementfactors of from 1.5 to 2.2, demonstrating that the porosity diffusionprocess increases the flow rate of the mobile phase under conditions ofcontinuous pressure or strain excitation.

This enhancement is also observed in a set of experiments where the sandis allowed to move from the exit port (screen is removed). Experimentswhere sand was allowed to exit are intended to simulate the behaviour ofwells producing heavy oil or other liquids by the process of sandproduction, discussed below in more detail. Results similar to thoseshown in FIG. 3 are obtained if the sand in the specimen is allowed toexit. Flow rate enhancement ratios of 2.0 to 2.5 are typically obtained.Typical results are shown in FIG. 4. The only difference in experimentalset-up between this figure and the previous one is that now the sand isallowed to flow out with the fluids at the exit port.

In the sand+liquid flow experiments (screen 28 removed), it was observedthat after some time the sand spontaneously stops exiting because of theformation of a stable sand arch behind the exit port 25. This blockagecauses the fluid exit rate to drop to a negligible value, <0.2 cm3/min,indicating that the sand grain arch is impeding the flow of liquids. Thepulsing and the strain perturbations overcame this blockage. The resultstherefore indicate that not only is there a basic flow rate enhancement,but also that the natural tendency of sand to create blockages can beovercome by pressure or strain pulsing, and if such blockages exist,they can be de-stabilized by pulsing. Clearly, this has substantialpositive implications on maintaining free fluid and sand flow to a wellproducing sand and liquids.

FIG. 5 shows the pressure response from the three pressure transducersin FIG. 2 (P1, P2, P3) when the device is subjected to a series ofcontinuous pressure pulses applied by manually squeezing the inflow hoseat point 29. As mentioned earlier, the actual magnitude of this pressurepulse is less than 0.2 kPa, and it has no effect on the average pressurehead applied to the sand pack. With continued pressure pulsing, however,the actual fluid pressure in the specimen begins to rise (the curvesswing upward); this is the effect of the porosity diffusion processbeing built up through the continuous excitation. When the pulsing isstopped, the pressure enhancement begins to decay slowly back to itsoriginal values, but the flow rate at the exit port drops to its initialvalues within 2-5 seconds. This suggests that fluid flow enhancementrequires continuous excitation. FIG. 5 shows that the pressure build upis less the farther away from the excitation source because the pressurebuild up attenuates as the porosity diffusion wave is transmittedthrough the system.

FIG. 6 shows details of the experimental set up where a small-embeddedacoustic transducer A1 (or several small transducers) is providingdynamic excitation. This excitation is of extremely small amplitude, yetit has the same effect as the pressure pulsing: it alters slightly thepressure in the fluid phase, and also changes the stresses between thegrains, which builds up the pressure in a way similar to FIG. 5. Thisalso is a porosity diffusion process because the acoustic excitation isa small-amplitude strain wave, which leads to small perturbations in theporosity of the porous medium. Experimental data show that this processalso leads to a fluid flow rate enhancement of the same order ofmagnitude as the pressure pulsing, and the enhancement effect can alsobe predicted and analysed theoretically.

4 The Physical Effect in Cold Production Wells

The proposed technology has wide applicability to a number of conditionsand cases. However, we believe that it has particular value in thepetroleum industry. Therefore, we describe in detail one productionprocess, Cold Production (CP), which will be substantially aided by theapplication of dynamic pressure or strain pulsing. This detailedpresentation is in no way meant to exclude any of the other possibleproduction practices for conventional oil, heavy oil, or other fluidspresent in porous media. This example was chosen because it has twomajor aspects of the beneficial effect of dynamic excitation throughpressure or strain pulsing: the effect of increasing basic flow rate,and the effect of breaking down the stable sand arches that form andtend to block oil flow.

4.1 Cold Production Mechanisms

It is best to have a clear understanding of the production mechanismsinvolved in the oil rate enhancement observed during Cold Production(CP) in order to understand how pressure or strain pulsing can enhanceflow rates and prevent blockages through the formation of sand arches.

First, movement of the solid matrix (sand) directly increases thevelocity of the fluid (oil+water+gas). Thus, sand movement increasesflow velocity, enhancing production. This can be seen in FIG. 4, wherethe initial slope of the flow line 39 when solids and fluids are bothallowed to flow is greater than for the case of no solids 37, even underthe same hydraulic head.

Second, sand extraction creates a more permeable zone around thewellbore through dilation of the sand matrix from an average of perhaps30% porosity to a porosity of 35-38% porosity. This zone grows in meanradius as more sand is produced (some wells produce in excess of 1200 cum of sand in their lifetime). If the growth of this zone is stopped orimpeded by sand blockages, flow rates will be lower. If stable sandarches form near the well perforations, the flow rates may drop to asmall fraction of their values when the sand is free to flow. If thesesand arches are continuously destabilized by dynamic excitation so thatthey cannot form in a stable manner, oil flow is not only morecontinuous, but it occurs at a greater rate.

Third, dissolved gas (mainly CH4) in the heavy oil exsolves gradually inresponse to a pressure drop. Bubble nucleation and gas exsolution isretarded in time because of low gas diffusivity in viscous oil. The gasalso tends to remain as a separate bubble phase during flow toward thewellbore, and bubbles expand as the pressure drops toward the productionsite, giving an internal drive mechanism referred to as foamy-flow. Itis believed that the foamy flow mechanism aids solids extraction andenhances fluid flow rate. The high viscosity of the oil retards gasexsolution during flow, and bubble mobility in the pores and throats isretarded by interfacial tensions. This alters permeability and enhancesdevelopment of small-scale tensile stresses, which help destabilize thesand.

Fourth, asphaltene precipitation and pore throat blocking by clays orfine-grained minerals are reduced during CP because of continuous solidsmovement, which liberates pore-blocking materials. Regular pulsing ofpressure or strain will greatly reduce the frequency of pore throatblockages, which may arise.

Oil production in CP wells can, exceptionally, be as high as 20-25cu.m/day, although 4-10 cu.m/day is more typical. After prolonged CP,done conventionally, rates as low as 1 or 2 cu.m/day can be acceptedproviding that initial rates were sufficient (e.g. >5 cu.m/day) for along enough period (e.g. 2 years) to warrant well drilling and fielddevelopment. However, the systematic application of pressure or strainpulsing is expected to extend the productive life of a well, and willalso increase the production rate of the well on a daily basis.

CP mechanisms depend on continued sand movement, which allows foamy oilmechanism to operate efficiently, and which allows continued growth of adisturbed, dilated, partly liquefied region around the well.

4.2 When Cold Production Stops

Some wells in Alberta have produced oil and sand stably for over 11years, with sand flow being successfully re-established after workovers,or even during production. However, some wells are extremely difficultto maintain on stable sand production. Generally, a failure to sustainsolids flow is directly related to a major drop in oil production.Therefore, re-establishment of sanding would have positive economicconsequences in increased oil rates or prolonged production periods.This re-establishment can be a consequence of a continuous destabilizingof the formation, unblocking perforations, or otherwise destroying anystable structures, which may have been generated in the sand. Dynamicexcitation, as described herein, is aimed at achieving these goals.

Stable sand structures are desirable, for good CP. These include: stableperforation sand arches which greatly retard fluid flow into the well;re-compaction of the sand in the near-wellbore environment; collapse andblockage of flow channels within the strata; or perhaps generation ofsome form of natural gravel-pack created by a natural settling aroundthe wellbore of the coarser grains in the formation. Changes of fluidsaturation leading to increases in capillary cohesion have beensuggested as a common blocking mechanism. This idea suggests that gasevolution leads to increasing gas saturation near the wellbore until acontinuous gas phase exists, with an apparent cohesion increase in thesand.

Little is known in detail about the actual blocking mechanisms becauseof difficulties in exploring the wellbore region and difficulties inlaboratory simulation, and therefore there is some difficulty over amethod of evaluation and implementing ameliorative measures. Whatmethods are used have been arrived at empirically and developed throughpractice. To our knowledge, no one uses pressure or strain pulsing of acontinuous nature during continued production.

Workovers have been used to perturb the formation and re-establish sandingress. The conventional methods used vary from surge and swaboperations to much more aggressive approaches such as Chemfrac (TM),involving igniting a rocket propellant charge to blow materials out ofthe perforations, as well as to shock the formation and perturb thesand. Considering the rise time and the fluid velocity, this method isprobably the most effective in unlocking perforations plugged with sandand small gravel particles. However, none of these methods arecontinuous in nature during the production of the well.

Mechanical sand bailers on wirelines are conventionally used to cleanthe well of sand before replacing a worn pump. The bailer is droppedrepeatedly into the sand until filled, and then withdrawn at arelatively rapid rate. This has a vibrational effect on the nearwellbore area, and a swabbing effect during withdrawal. Often, afterbailing, sand has flowed back into the well through the perforations,and cases have been reported of six to eight days of bailing, removingas much as 1-3 cu.m of sand; that is, 10-15 times the amount that was inthe wellbore in the first place. Bailing is relatively successful inre-establishing sanding, but extensive periods of bailing are clearly tobe avoided if better alternatives exist.

Injection of various chemical formulations to break capillary effects isrelatively common, as is injection of several cubic meters of heatedoil. These methods are thought to break any apparent (capillary)cohesion in the sand, and the outward flow is thought to reopen someperforations that may have become blocked.

Thus, although many conventional wells produce sand freely, blockagesoccur. The method of strain or pressure pulsing, as described herein,through the process of porosity diffusion, can provide long-termcontinuous production at an enhanced flow rate by activating the ambientstress field dynamically. This process can destroy small-scale stablesand arches and keep pore throats open. Blocking materials such asasphaltenes and clay particles are much less likely to plug pore throatsunder conditions of dynamic pressure or strain excitation.

5 Field Configurations

FIGS. 7a and 7 b show an example of how dynamic enhancement throughpressure pulsing can be implemented in the field. A pressure pulsingsystem is installed in the central well 40 of a porous stratumcontaining oil and water. Perforations in the steel casing 42 of thewell 43 allow full and unhindered pressure communication between theliquid in the wellbore and the liquids in the pores and fractures of theporous medium. The well is completely liquid-filled between the pulsingdevice and the perforations, and is maintained in that condition.

A number of adjacent wells (H1, H2, H3, and H4) are producing fluids andtherefore have a well pressure that is less than the excitation well 40.In other words, the pressure gradient in the porous medium is directedby the induced pressure differences so that fluid flow is toward theproducing wells. FIG. 7b shows a typical pressure decline curve betweenthe excitation well and the producing wells. The distance d between thewell 40 and the producing wells 43 is dictated by the physicalproperties of the medium (compressibility, permeability, fluidviscosity, porosity, thickness, fluid saturation), and must bedetermined through calculations and field experience for individualcases. The pattern shown, or any other suitable pattern of producingwells and excitation wells, may be repeated to give the necessaryspatial coverage of a producing field.

In the field, the amplitude, frequency, and waveform of the dynamicexcitation can be varied to find the optimum values required to maximizethe dynamic enhancement effect. Because porous media have certaincharacteristic frequencies at which energy dissipation is minimal,analysis, laboratory experimentation, and empirical field optimizationmethods (based on outflow rates at the producing wells and othermonitoring approaches, discussed below) might be required to find thebest set of operating parameters which maximize the dynamic flow rateenhancement. Monitoring approaches for optimizations are discussedlater.

FIG. 8 shows another possible configuration for implementation ofpressure or strain pulsing to enhance fluid flow to wells. Forillustration purposes, suppose that a vertical well 45 is completed witha number of short-radius laterals 46, each of which is considered ahorizontal well. Fluid is to be withdrawn through the well 45 with thehorizontal drains. A number of excitation wells 47 are emplaced abovethe horizontal laterals, and pressure pulsing or strain pulsing isapplied in these wells through excitation devices 48.

In both cases pulsing can be generated either through a downhole or asurface pressure pulsing which can be activated by mechanical, hydraulicor pneumatic means.

6 Pressure and Strain Pulse Devices for Oil Exploitation

FIG. 9 shows one example of a pressure pulsing device that causes aperiodic pressure excitation at a controllable frequency and amplitude.The pressure pulsing can be varied in frequency (number of pulses over atime interval), in amplitude (magnitude of the pressure pulse), and inwaveform (the shape of the pressure pulse). The pulsing is governed fromthe surface through an appropriately designed electronic or mechanicalcontrol system. The major elements of the diagram are:

a) A wellbore 50, having a casing 52, embedded in cement 53, perforatedinto the target formation 54.

b) A piston pump barrel 56 which, when mechanically actuated, generatesa pressure pulse.

c) A one-way valve 57 to allow entry of fluid into the zone below thepiston pump on the upstroke of the piston.

d) An actuating device, in this drawing represented as a rod 58 tosurface within the production tubing 59 that is isolated from the casingannulus with a packer 60. This driving mechanism can be varied infrequency and stroke length (volume).

The driving mechanism for the piston pump 56 in FIG. 9 is asurface-driven reciprocal or rotary mechanical drive that creates anup-and-down motion of the piston 56. Alternatively, the drivingmechanism can be an electromechanical device above the piston pumpdriven by electrical power. Alternatively, a surface pressure impulsecan be applied through the tubing. In this case, the piston pump may bereplaced by a flutter valve top-hole or bottom-hole assembly which opensand closes to create pressure surges which enter the formation 54through the perforations, but does not affect the annulus pressurebecause of the packer 60.

The piston 56 may contain the one-way valve 57 to allow intake of fluidon the upstroke, and expelling the incremental fluid on the down stroke,generating the pressure pulse. Alternatively, the fluid valve 57 can beclosed, and a periodic pressure impulse generated with a closed system.

As shown in FIGS. 10a, 10 b, and 10 c, a single well 62 is producingfluids through perforations in the steel casing 63 because the pressurein the well is maintained at a value lower than the fluid pressure inthe far-field, generating a pressure gradient which drives fluids (or afluid-solid mixture) to the wellbore 62. The examples show both aninclined well and a vertical well integrated with progressive cavitypump system for purposes of illustration only. Operational descriptionswill focus on a rotating elliptical mass, but it is understood that theprinciples apply to other pulse-like sources of strain energy.

FIG. 10a shows a typical down-hole assembly for the application of aperiodic mechanical strain to the casing in the producing formation, andthe cemented casing serves as a rigid coupling system that transmits theperiodic straining to the formation. The major elements of the diagramare:

a) A cased 63 cemented wellbore perforated into the target formation 64with tubing assembly and other peripheral devices.

b) A fluid pump 65 to withdraw fluids and sand from the wellbore 62.

c) Housings and devices that couple the fluid pump 65 to the tubing andif desired to the well casing 63, through a rigid packer (not shown).

d) A system of rods 67 connecting the fluid pump to the drive mechanism.

e) A drive mechanism to give rotary action to the fluid pump andeccentric mass 68.

f) An eccentric mass 68 which is mechanically linked to the fluid pump65 (FIG. 10c).

Installed in the wellbore is a mechanical or electromechanical devicethat applies vibrational energy to the casing through rotation of aneccentric mass or through volumetric straining. The device is fixed tothe exterior casing 63 through conventional means, using a packer withsteel contacting pads (slips) or other means whereby the vibrationalenergy is efficiently transmitted to the steel casing with a minimum ofenergy losses. A schematic cross-section of a rotating elliptical massis given in FIG. 10c. The central square hole is stabbed by a square rodon the bottom of the power rods 67, which are rotated from the surface.As the rods rotate and thereby also activate the fluid pump 65, theeccentric mass is rotated at the same angular velocity, or else thevelocity may be less or greater if a mechanical gearing device isincluded.

The rotation of the eccentric mass 68 creates an imbalance of force,which causes the casing 63 to apply a rotational strain to thesurrounding porous medium through which the casing penetrates. Therotational strain generates an outward moving porosity diffusion wavethat perturbs the liquid in the porous medium, causing an accompanyingpressure pulse in the liquid. The energy thereby applied to the liquid(and entrained mobile solids) in the porous medium leads to anenhancement of liquid flow into the wellbore, irrespective of thedirection of propagation of the porosity perturbation. Furthermore, thestrain energy thereby applied reduces or eliminates tendencies for thematerial pore throats or fractures to become blocked by fine-grainedparticles, precipitants, or through the formation of stable granulararches. The fluid produced is removed from the wellbore through the pump65, which in this example sits above the elliptical rotating mass, butthe order of the devices may be altered. Both the pump and the rotatingmass may be mechanically driven, electrically driven, or one may bemechanical and the other electrical.

FIG. 10b shows a typical down-hole assembly for the application of aperiodic mechanical strain to the casing in the producing formation, andthe cemented casing serves as a rigid coupling system that transmits theperiodic straining to the liquid in the formation. The major elements ofthe diagram are:

a) A cased cemented wellbore 69 perforated into the target formation 70with tubing assembly 72 and other peripheral devices.

b) A progressive cavity (PC) pump 73 to withdraw fluids and sand fromthe wellbore 69.

c) Housings and devices that couple the stator of the PC pump 73 to thetubing 72 and if desired to the well casing, through a rigid packer, notshown.

d) A system of rods 74 connecting the PC pump to a drive mechanism 75.

e) A drive mechanism 75 to give rotary action to the PC pump andeccentric mass 76.

f) An eccentric mass 76 which is mechanically linked to the PC pump.

The driving mechanism for the PC pump 73 in FIG. 10b is a surface-drivenrotary mechanical drive that creates a variable frequency rotation ofthe rods 74, rotor, and the eccentric mass 76. Alternatively, thedriving mechanism for the bottom-hole assembly can be anelectromechanical device located above or below the rotor, and driven byelectrical power.

The device that applies a large rotational strain to the casing, is aneccentric mass driver 76, which is rigidly coupled to the rotor of thepump 73. The strain is a circular impulse triggered by rotation of amass that is located off the centre of rotation of the PC pump assembly,and it may be located above or below the rotor. To transmit the strainseffective to the well casing, it is necessary that the rotatingeccentric mass be rigidly coupled to the casing. This is achievedthrough a packer seating assembly (not shown) either below or above thePC pump, but close to the eccentric mass, so that the rotary impulse isefficiently transmitted.

FIG. 11 shows an approach to transmit periodic mechanical energy downthe tubing assembly in a cased well through application of mechanicalexcitation at the surface. These strains are transmitted to the bottomof the well, where they may be converted to a pressure pulse, ormechanically linked to the casing to transmit mechanical strains to theliquid in the formation. The major elements of the diagram are:

(a) A cased cemented wellbore 78 perforated into the target formation(not shown).

(b) A tubing and rod assembly.

(c) A drive head 79 that rotates the rod to provide motive power to thebottom-hole fluid pump (not shown) which may be a progressive cavitypump or a reciprocating pump.

(d) A packer device 80 to allow the polished section of the tubing 82 toundergo a periodic vertical movement independent of the casing or therods.

(e) A driving mechanism 83 of variable frequency and stroke that impartsa vertical periodic motion to the tubing 82, separate and distinct fromthe pump drive-head 79.

(f) A set of reaction springs 84 and a flange 85 on the wellhead to actin unison with the tubing drive mechanism 83 to give the periodicvertical movement.

(g) Housings and devices that isolate yet allow the movement of thetubing and rods to allow production from the well while tubingexcitation is active.

The example shown in FIG. 11 is a rotating motor actuating the tubingthrough an eccentric cam, with counter-stroke reaction provided by a setof springs. A variety of other driving mechanisms can be used, includinga direct mechanical linkage of a reciprocating device to the tubing(perhaps eliminating the springs).

7 Pressure or Strain Pulsing in a Reaction Bed

A reaction bed (FIG. 12) of granular or porous material 86 is used tofoster chemical interaction by introducing two fluid species(liquid-liquid or liquid-gas). The pore-and-throat structure similar tothat in FIG. 1 of the porous medium helps break up the two fluids intointermingled phases with a large surface contact area, which acceleratesthe reaction process. The solid phase may, for example, be an inertmaterial such as silica particles, or it may be a bed of particles ofcatalyst or of ceramic particles coated by a catalyst. In the case of acatalyst, the use of a porous bed gives a high surface contact areabetween the catalyst and the reacting phases. The flow through thesystem is achieved either through downward gravitational flow, orthrough a difference in the fluid pressure between the input and exitports. The flow in this case may be in any direction, but always in thedirection of the induced pressure gradient. In the example shown, flowis from top to bottom. To increase the efficiency of the process, theflow rate of the fluids through the reaction bed should be maximized.

Fluid rate flow is accomplished through the application of pressurepulses on the reaction bed by pulsing the pressure in the liquid inflowlines (S1, S2) or exit lines (S3), or by applying pressure pulsesthrough a port (T) or ports in liquid (pressure) communication with thepermeants. Alternatively, vibrational strain energy can be appliedeither externally or internally (U1-U4) through the use of mechanicaldevices or electromechanical transducers. The symbol inside the smallcircles indicates that pulsating pressure or strain is being applied atthese points.

In these cases, porosity diffusion processes and the coupledpressure-strain responses create the necessary flow enhancement effect.

8 Pressure or Strain Pulsing to Facilitate Aquifer Remediation

We give the example of cleaning of a potable water aquifer that has beencontaminated by a non-wetting phase, which has permeated the pores andexists as a continuous liquid phase. Using strategies, which, forexample, may be of similar configurations to those in FIGS. 7 and 8, anddevices presented in FIGS. 8 to 10 b, pump-out wells are configured togive the best areal coverage of the contaminated water reservoir.Furthermore, excitation leading to fluid flow enhancement throughporosity diffusion effects at these shallow depths can be implemented aswell at the surface, through the use of harmonic oscillators, forexample (not shown).

The aquifer clean-up proceeds by continued pumping and can also beenhanced by the input of water or other suitable liquid or solid/liquidmixtures at the excitation wells, or at other wells installedspecifically for this purpose. The key aspects in this case are thecontinued excitation, the continued provision of a source of liquid toaccount for the voidage generated by pumping the wells, and themaintenance of a pressure gradient in the aquifer that maintains flow tothe low pressure production (clean-out) wells.

9 Monitoring and Optimization in the Field

Periodic straining or pulsing can enhance the flow rate in a porousmedium. The excitation gives rise to dynamic porosity diffusion effects.Optimization of the excitation process involves determining the mosteffective frequency, amplitude, and waveform to be applied. Control ofthe excitation is applied through a controller and a power source, withan oscilloscope or other read-out device to examine the characteristicsof the excitation.

In order to optimize the process, it is necessary to monitor both theexcitation effects and the production rate. This is achieved throughmonitoring production rates using flow meters or tank gauges, andthrough monitoring the transmission of the excitation within thereservoir. The important excitation factors to monitor are the nature ofthe excitation and the nature of the waves transmitted through thereservoir, and these data are collected at a data acquisition systemconnected to a computer. The parameters of importance in the reservoirare the pressure and the wave trains. The pressure is monitored at anumber of points through pressure ports in observation wells andexcitation wells, and the wave train is monitored using geophones,accelerometers, or other suitable devices placed in observation wells,excitation wells, or behind the casing in production wells.

In order to optimize the process, the data streams are taken to acentral computer where the data are plotted and correlated. Then, theparameters are optimized to allow maximization of the production rate,subject of course to the limitations of the equipment used for theexcitation.

10 Criteria for Site Selection

The preferred framework for field implementation of dynamic enhancementis outlined below. It is designed to answer a number of basicrequirements to facilitate proper site selection, which should increasethe probability of successful implementation and oil recovery.

10.1 Reservoir Porosity

The effect of vibrational enhancement is relative to the currentparameters, which make economic recoverability viable. For example,porosity simply determines the amount of oil in the reservoir. It doesnot, in theory, play a direct role in the effectiveness of the processuntil large porosity values are obtained. It is suggested that formaximum effectiveness the bounds of porosity range from 18% to 35%. Atporosity levels above 35% the effects dynamic enhancement becomes lesscumulative, diminishing with further increases. Below about 18% (i.e oilshale), enhancement by pulsing would not be expected to occur.

10.2 Minimum and Maximum Porous Media Thickness

An aim of dynamic enhancement through application of pressure or strainpulses, as described herein, is to propagate a slow moving wave inthree-dimensional space. This may be in an oil reservoir or in a systemcomprised of a natural or artificial porous media. For optimumoperation, the preferred constraints on propagation of a continuous orepisodic pressure or strains in the systems described previously are asfollows:

a) For oil reservoirs and aquifers a minimum thickness of 3.0 meters toa maximum of 50.0 meters.

b) For contained reaction beds, a minimum thickness of 0.20 meters to amaximum of 1.0 meters.

10.3 Caprock

Caprock, the geomaterial that overlies an oil reservoir or aquifer,serves two purposes. First, it prevents the pressure or strain pulsefrom upward propagation beyond the parameters outlined in Section 10.2,and it prevents upward flow of fluid. A caprock may consist of shale,dolostone, salt (or other evaporites), very dense clays, tightlimestones, and so on. The key element for a caprock in the case ofpressure or strain pulse propagation is that it be of extremely lowpermeability (e.g salt), or have very low permeability (e.g shales,dolostone, and very dense clays). It is important to note that thepropagation of the pressure or strain pulse propagates through theliquid in the porous medium. It is the elastic properties of the matrixand the mobility and compressibility conditions of the fluid, which willultimately determine the viability of the process. If the matrix isweak, or brittle, the matrix might tend to crack and consolidate underthe action of pulses that have enough energy to create the dynamicenhancement of liquid flow rate as described herein. In that case, theinvention would be contra-indicated. The caprock conditions are of asecondary nature but are listed here for completeness.

10.4 Permeability

The ratio of viscosity to permeability defines the mobility of the oilin a reservoir, a contaminant in an aquifer, of fluid in a reaction bed.The range of permeability for aquifers and bed reactors preferablyshould be on the order of 1000 sq.cm (gravel) to 0.01 sq.cm (silt). Forlight oil and heavy oil reservoirs the dynamic enhancement process isviable at a range from 10⁻¹¹ cm2 to 10⁻¹³ cm2.

10.5 Viscosity

The magnitude of the diffusion constant and the scale of the interactiondetermine the speed of the pressure or strain pulse. The diffusionconstant is directly proportional to permeability divided by viscosity.From our calculations of the speed of propagation of a pressure orstrain pulse without the advantage of large tectonic stresses in theearth or large hydraulically induced stresses (i.e. bed reactors) weplace the cutoff at 30 API gravity. When the earth's tectonic stressescan be used as an energy source both grain slippage and fluid flow willeffect the propagation speed of the pressure or strain pulse. In thiscase, and in the case of high hydraulic stresses, the cutoff to oils canbe as low as 10 API gravity.

11 Estimation of Enhanced Fluid Production from a Pulse Series

It has sometimes been observed, after an earthquake, that the flow rateof liquid through a porous medium has been significantly improved, atleast for a time. This has led to techniques and proposals forsubjecting the porous structure to artificial seismic perturbations.However, the technique of applying pulses to the liquid in the porousmedium is quite different from the technique of imparting seismicperturbations to the medium itself, being much less disruptive (and lesscostly). Besides, although seismic operations might open up the pores,it might happen instead that the medium consolidates and closes thepores; the system as described herein is aimed rather at pulsing theliquid (and any grains that might be entrained in the liquid) relativeto the solid matrix, not at pulsing or shaking the solid matrix itself.

A quantitative estimation of the cumulative enhancement of fluidproduction, which is observed in porous media subjected to a periodicimpulse, depends on the geometric disposition between the pulsegenerator and the production wellbore. Such a quantitative estimate canbe achieved for an arbitrary geometry through numerical calculationsbased on the pressure pulse and a porosity diffusion model forearthquake sources or explosive perturbations. Those perturbationsproduce irreversible changes in porous media, i.e. fracture, dilatancyand compaction. Any impulse-triggered decrease of porosity leads toeffective compaction, and this can squeeze an additional amount of fluidfrom the porous medium. From a physical point of view this mechanism isclear, and such a mechanism is known to lead to excess pore pressuresand sand liquefaction during strong earthquakes.

In contrast to the irreversible compaction arising from single strongperturbations, the invention is aimed at providing reversible strainsarising from continuous weak perturbations. Each perturbation (e.g.tapping or short-term cyclic straining) is assumed to be of an elasticnature which does not produce any residual, irreversible deformation,but does cause a periodic perturbation in the porosity of the systemthrough compression and relaxation.

In the aftermath of an impact, a porous medium relaxes to theequilibrium state in a diffusional manner because the relaxation processinvolves flow of the viscous saturating fluid with respect to the porousskeleton. If we apply another perturbation before the proceeding onefully decays, while withdrawing the produced fluid through a port, acumulative, synergetic effect can be achieved. A quantitative estimationof this effect for specific cases involving non-symmetric dispositionsof the perturbation source and the wellbore requires extensiveanalytical and computer model calculations based on numerical methods.This approach, however, tends to obscure the physical logic on which themodel is based.

12 Further Considerations

An aim of the invention is to apply pressure pulses and strain pulses toa liquid in natural and man-made porous media to enhance the flow rateof the mobile fluid phases and to diminish the probability of flow-rateimpairment through the internal bridging of particles. The approach hasbeen verified theoretically, in the laboratory, and through empiricalobservations in field situations in the petroleum industry and for waterwells. A key element is the concept of porosity waves and attendantpressure pulses, which travel through the medium by diffusionalprocesses. To our knowledge, this phenomenon has not been previouslyidentified in such media and considered for the purposes of fluid flowrate enhancement. Applications are envisioned particularly but notexclusively for the petroleum industry and the chemical processingindustry. Also, in reservoirs contaminated by non-aqueous phase,non-wetting liquids, implementation of pressure pulsing and other meansof generating porosity diffusion enhanced flow is expected to accelerateclean-up operations, and make them more effective.

The techniques as described herein should be distinguished fromfluidized bed technology, in which a granular material is pulsed at suchan energy level that the whole solid matrix is in a state of heavingmotion. In the present case, the intention is that the solid matrix doesnot move, but rather that the pulses pass through the liquid while thesolid matrix remains substantially stationary.

Liquid flowing through a porous medium has a flow rate, which depends onthe impressed pressure differential. Within the porous medium, thevelocity of the liquid, as caused by that impressed pressuredifferential, will vary from pore to pore, but the velocity may beaveraged as a volumetric flow rate over the whole treatment volume.

Considering a pore P: if the porosity of pore P should decrease, i.e ifthe pore should close up, the velocity of liquid passing through thatpore would go down, for a given impressed pressure differential. Theporosity might go down if, for example, a grain of sand might becomesnagged in the pore.

The pressure pulses spread through the liquid, as a wave-front, with awave velocity. The wave front velocity (and magnitude) will not be thesame at every pore in the treatment volume. The velocity of propagationof the wave-front may be averaged over the treatment volume.

In a real porous medium, the average velocity of propagation of thewave-front will be much faster than the average flow-through velocity ofthe liquid. Similarly, at each pore, the velocity of propagation of thewave-front will be much faster than the velocity of the liquidtravelling passing through the pore.

The pressure pulse, as it passes through a pore, causes a surge in theliquid present in the pore. As the wavefront passes, the pressuredifferential across the pore increases, and so the through-flow velocityof the liquid in the pore momentarily speeds up (assuming the wave-frontis travelling in the same direction through the pore as the liquid).Afterwards, the pressure differential across the pore drops back, as thewavefront passes, and the liquid in the pore slows down and reverts backto the background velocity of the liquid through the pore.

If the wavefront were travelling against the liquid travel velocity, thepulse would cause the velocity of the liquid in the pore to dropmomentarily, then gradually speed up again to the background velocity,as the pulse passes. In some cases, the velocity of the flow of liquidin the pore might even reverse (and back flush the pore) momentarily.

It is the sudden changes in the through-velocity of the liquid in thepore that prevents grains settling in the pore, whether the pulses causea momentary speeding up of the liquid in the pore, or a momentaryslowing down (or even reversal) of the liquid in the pore.

Thus, the pores are kept open by the surges. The sudden change invelocity of the liquid dislodges or flushes away grains that might besnagged in the pores, and prevents grains from snagging in the pores. Itmay be noted that an actual reversal of the flow velocity of the liquidcan be especially effective, by back-flushing the pores clear. Bysweeping or flushing the pores clean, the flow rate of liquid throughthe treatment medium can be increased; or, at the least, the rate atwhich the pores become clogged can be slowed.

An even more beneficial ratcheting effect also can be engineered. Thepulses have a specific wave form, which includes a gradual rise inpressure, followed by a gradual fall in pressure. See FIG. 5. (The waveform at pore P might not be the same as the wave form as created by thepulse generating means.) Insofar as this pressure pulse gives rise to achange in the pressure differential across the pore, the velocity of theliquid in the pore undergoes a change that follows a similar waveform.

If the pulses are infrequent, the next (junior) pulse reaches the pore Pafter the earlier (senior) pulse has died away, and so each pulse ofpressure has an independent, i.e non-cumulative, effect on thethrough-velocity of the liquid passing through the pore. This conditionis illustrated in FIG. 14a. However, if the pulses are more frequent,the junior pulse might reach the liquid in the pore before the seniorpulse is finished. That is to say: the senior-surge in the flow rate ofthe liquid through the pore is still present when the junior-surge inthe flow rate arrives. The senior-surge in liquid flow rate is caused bythe pressure differential imposed by the senior pulse, and thejunior-surge in liquid flow rate is caused by the pressure differentialimposed by the junior pulse.

With the arrival of the next pulse after that, the velocity of the flowof liquid in the pore is given a further incremental increase, and soon. This condition is shown in FIG. 14b.

The effect is repeated in all the other pores, and thus the effect ismanifested as an increase in the overall flow rate of the liquid throughthe treatment volume of the porous medium. It has been found that thevelocity of the flow of liquid through the treatment volume can beincreased asymptotically to an upper limit 93 (FIG. 14b), which isconsiderably faster than the background flow rate 94 arising simply fromthe differential pressure imposed on the treatment volume withoutpulsing. That is to say: the flow rate is increased by the pulsing as ifa larger pressure differential had been imposed, or as if the porosityhad been increased.

Thus, not only does the pulsing as described herein tend to keep thepores clear as the changes in flow velocity flush the pores, but alsothe pulsing, if done at the right frequency, can increase the actualflow rate of the liquid through the treatment volume.

The frequency of the pulses should be rapid enough that a junior pulsearrives at the pore before the senior pulse has died away. On the otherhand, the frequency of the pulses should not be too rapid. Too high afrequency might set up resonances in the solid matrix material, andcause the material to undergo an amplitude of movement that might causedamage. Also, the higher the frequency, the more it becomes difficult toget enough energy into each pulse to actually cause a significantpressure surge in the liquid, per pulse.

The engineer should carry out tests at the treatment site, in which theoverall through-flow rate is measured for different frequencies ofpulsing. The frequency should be increased (starting from about 1 Hz)until a frequency is reached beyond which no further increase inthrough-flow rate is achieved. Typically, that happens when thefrequency of pulsing is in the range 1 Hz to 10 Hz.

The magnitude or energy of the pulses is important. If the energy of thepulses is too high, the solid matrix material can be damaged. That is tosay, the matrix material should not be shaken so vigorously as to causesome consolidation of the material, which would thereby lose someporosity and permeability. The energy should be high enough, though, tomake the momentary change in the velocity of the liquid passing throughthe pores significant.

It will be understood that, in many cases, the liquid flowing throughthe pores will have some sand or other solid grains entrained in theflow. The sand grains of course come from the solid material making upthe matrix. The movement of the sand grains, entrained in the movingliquid, should be distinguished from consolidation of the matrix, whichinvolves a settling movement of the matrix material.

The direction of the pulses is important. In some case, for example ifthe pulses are generated actually in the extraction well (as in FIG.10b, for example) the wave-front of pulses propagates in the directionaway from the extraction well. In that case, the change in pressuredifferential across the pore, due to the pulse, acts to create amomentary velocity which opposes the velocity of the liquid through thepore towards the extraction well, due to the imposed background pressuredifferential. It might be possible in that case, by adjusting thefrequency of the pulses, actually to reduce the flow rate of the liquidthrough the pores, i.e to impose on the liquid such a cumulative effectupon the velocity or flow-rate that the pulse-created flow-rate opposesthe background flow-rate. Of course, significantly dropping theflow-rate would run counter to the aims of the invention, and theengineer should see to it, when operating a system in which thewave-front velocity is in the opposite direction to the liquid flow-ratevelocity, that the frequency of pulsing stays out of the range in whichflow of the liquid towards the extraction-well might be seriouslyattenuated. The ratcheting of flow velocity as shown in FIG. 14b onlyapplies when the pulses are travelling in the same direction as theliquid.

By correctly setting the pulsing frequency, the pulsing can be used toprevent clogging of the pores, by flushing the pores and resisting thepossible snagging of grains in the pores, whether the wave-frontvelocity is with or against the liquid extraction velocity.

One of the dangers of using a separate excitation well to generate thepulses is the possibility of inadvertently establishing a preferredpathway through the porous material, from the excitation well to theextraction well. If that happens, the well would be finished, in thatnow the liquid being pulled out of the extraction well is simply theliquid being fed in at the excitation well.

A separate excitation well is useful in that the engineer will find iteasier to create the type of pulses that will make a significantdifference to the flow rate of the liquid if he not only provides aseparate excitation well, so that the direction of the pulses reinforcesthe flow-rate of liquid towards the extraction well, but also if heinjects a (small) charge of liquid into the excitation well with eachpulse. Injecting a charge of liquid at each pulse delays the drop-off orfall-back of flow-rate velocity after the pulse passes, which makes iteasier to achieve the ratcheting of the pulses that can create asignificant improvement in flow rate.

However, as mentioned, when using an excitation well, the engineer mustmake sure he does not kill the production well. It is recognised thatthe pulses can be made to travel considerable distances through theporous medium; sufficiently far indeed that the excitation well can beplaced far enough away that the danger of killing the well becomesnegligible, and yet the pulses can be made to penetrate large distancesinto the porous medium.

It is emphasised that the pulses are pulses of pressure passing throughthe liquid; the pulses do not require the solid matrix material to move.(Of course, if the liquid pressure changes, a pedant might argue thatthe solid matrix must undergo distortions corresponding to the change inpressure, if only very slightly. But the invention is concerned withreal practical effects, and the pulses as described herein can, as amatter of substance, be generated, and can perform the useful functionas described, even if the solid matrix notionally did not move at all.)

In the case where the pulses are generated as pressure pulses, thepulses are generated by creating motion directly in the liquid; in thecase where the pulses are generated as strain pulses, the pulse is firstapplied to a local region of the solid matrix material, and onlyindirectly thereby to the liquid. In that case, the solid matrixmaterial undergoes, or might undergo, a measurable strain in launchingthe pulse into the liquid. However, such a strain would be verylocalised, as to the distance of penetration of the strain into theporous medium, whereas the pulse that such strain creates in the liquidwould then penetrate much further into the porous medium, through theliquid.

What is claimed is:
 1. A procedure for increasing the permeability ofground material surrounding a borehole in the ground, wherein theprocedure includes: providing a substantial charge-volume of acharge-liquid in the borehole; providing an operable charging-means,which is effective, when operated, to discharge the whole of thecharge-volume radially outwards, as a coherent volume, at a substantialvelocity, from the borehole into the surrounding ground material;operating the charging-means for a charge-period, thereby causing thecharge-volume of the charge-liquid to flow outwards from the boreholeinto the surrounding ground material; providing an operable suck-backmeans, which is effective, when operated, to forcefully suck liquid fromthe surrounding around material into the borehole, at a substantialvelocity; operating the suck-back means during the recovery-period,whereby at least some of the charge-liquid returns into the boreholeduring the recovery-period; pulse-operating the charging-means with thesuck-back means, by operating the charging-means and the suck-back meansalternately, in a pulsing manner; continuing to pulse-operate thecharging-means with the suck-back means for a sufficiently long timethat the permeability of the ground material surrounding the borehole issubstantially increased.
 2. Procedure of claim 1, includingpulse-operating the charging-means at a frequency that is fast enough tocause a progressive increase in the liquid flow-rate velocity with eachpulse.
 3. Procedure of claim 1, including pulse-operating thecharging-means in such manner as to generate the pulses in the liquidsubstantially without generating distortions of the surrounding aroundmaterial.
 4. Procedure of claim 1, wherein the charge-liquid is oil. 5.Procedure of claim 1, wherein the charge-liquid is water.
 6. Procedureof claim 1, wherein the charge-volume, as wholly discharged into thesurrounding ground upon operating the charging-means, is at leastseveral milli-liters.
 7. Procedure of claim 1, wherein the procedureincludes continuing to pulse-operate the charging-means at a frequencyof 10 Hz or slower.
 8. Procedure of claim 7, wherein the procedureincludes continuing to pulse-operate the charging means at a frequencyof 1 Hz or slower.
 9. Procedure of claim 1, wherein the charging-meansincludes a cylinder and a relatively moveable piston, and the cylinderincludes a port, which is in liquid-transfer-communication with theground surrounding the borehole; and the procedure includes placing thecharge-volume of the charge-liquid in the cylinder, and forcefullydriving the moveable piston, thereby forcing the charge-volume of thecharge-liquid through the port, and out into the surrounding groundmaterial.
 10. Procedure of claim 1, wherein the procedure includesproviding a means for supplying extra charge-liquid, and making up thevolume of charge-liquid to the charge-volume, each pulse.
 11. Procedureof claim 1, wherein the charging-means includes a cylinder and arelatively moveable piston, and the cylinder includes a port, which isin liquid-transfer-communication with the ground surrounding theborehole, and the procedure includes the steps: of placing thecharge-volume of the charge-liquid in the cylinder, and forcefullydriving the moveable piston, thereby forcing the charge-volume of thecharge-liquid through the port, and out into the surrounding groundmaterial; of providing an operable piston-withdrawal means, andoperating same to forcefully withdraw the piston, to create a suction inthe cylinder, and thereby to suck at least some of the charge-liquidback through the port.
 12. Procedure of claim 11, which includes waitingfor a suitable time, after operating the piston-withdrawal means to drawthe piston back, for at least some of the expelled liquid to drain backinto the cylinder, and of then admitting a make-up volume of the chargeliquid, to refill the cylinder to the charge-volume.
 13. Procedure ofclaim 11, including preventing substantially all the explelled liquidfrom returning into the cylinder, and admitting a fresh charge-volumeinto the cylinder, each pulse.
 14. Procedure of claim 1, wherein theprocedure includes continuing to pulse-operate the charging-means for apulsing-period of several days.
 15. Procedure of claim 1, wherein theprocedure is effective, when carried out, to increase the permeabilityof the ground material around an extraction well, being a well forextracting a value-liquid from the ground, and thereby to increase therate at which the value-liquid can be extracted from the extractionwell, after the procedure has been carried out.
 16. Procedure of claim15, wherein the borehole in the ground is located close to, but spacedfrom, the extraction well.
 17. Procedure of claim 15, wherein theborehole in the ground is one with the extraction well.
 18. Procedure ofclaim 17, wherein the procedure includes: continuing to pulse-operatethe charging-means for a pulsing-period of several days; then ceasing tooperate the charging-means; then removing the charging-means, to theextent necessary to make the extraction-well ready for extracting thevalue-liquid from the well; and then proceeding to extract thevalue-liquid from the well.
 19. Procedure of claim 1, wherein theprocedure includes the step of varying the charge-period and therecovery-period, during the pulsing period.
 20. Procedure of claim 1,wherein the procedure includes operating the charging-means continuouslyduring the charge-period, in that, once discharge of the charge-volumehas started, the whole charge-volume is discharged without interruption.